Bispecific antibodies (bsAbs) can simultaneously bind two different antigens or epitopes. Their dual-targeting capability enables novel mechanisms of action, gaining therapeutic advantages over conventional monospecific mAbs. In recent years, the number of bsAbs grows rapidly and bsAbs under development are available in diverse formats. In particular, Fc-containing IgG-like bsAbs, which represent the major group, can be constructed in asymmetric or symmetric format. For asymmetric ones, whose assembly requires multiple distinct chains, although numerous strategies have been developed to promote desired chain pairing, product-related variants such as free chains, half molecules and mispaired species are usually present at various levels. For symmetric ones, increased level of aggregates and truncating variants is often associated with their production. In general, bsAbs pose greater challenges to the downstream team than regular mAbs. In the past few years, our team successfully developed the downstream process for over 70 bsAbs in greater than 30 different formats and accumulated substantial experience. This review introduces general strategies that we have used while purifying these challenging molecules.
{"title":"General strategies for IgG-like bispecific antibody purification.","authors":"Yifeng Li","doi":"10.1002/btpr.3515","DOIUrl":"https://doi.org/10.1002/btpr.3515","url":null,"abstract":"<p><p>Bispecific antibodies (bsAbs) can simultaneously bind two different antigens or epitopes. Their dual-targeting capability enables novel mechanisms of action, gaining therapeutic advantages over conventional monospecific mAbs. In recent years, the number of bsAbs grows rapidly and bsAbs under development are available in diverse formats. In particular, Fc-containing IgG-like bsAbs, which represent the major group, can be constructed in asymmetric or symmetric format. For asymmetric ones, whose assembly requires multiple distinct chains, although numerous strategies have been developed to promote desired chain pairing, product-related variants such as free chains, half molecules and mispaired species are usually present at various levels. For symmetric ones, increased level of aggregates and truncating variants is often associated with their production. In general, bsAbs pose greater challenges to the downstream team than regular mAbs. In the past few years, our team successfully developed the downstream process for over 70 bsAbs in greater than 30 different formats and accumulated substantial experience. This review introduces general strategies that we have used while purifying these challenging molecules.</p>","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":" ","pages":"e3515"},"PeriodicalIF":2.5,"publicationDate":"2024-10-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142457094","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Tryptamines play diverse roles as neurotransmitters and psychoactive compounds found in various organisms. Psilocybin, a notable tryptamine, has garnered attention for its therapeutic potential in treating mental health disorders like depression and anxiety. Despite its promising applications, current extraction methods for psilocybin are labor-intensive and economically limiting. We suggest biocatalysis as a sustainable alternative, leveraging enzymes to synthesize psilocybin and other tryptamines efficiently. By elucidating psilocybin biosynthesis pathways, researchers aim to advance synthetic methodologies and industrial applications. This review underscores the transformative potential of biocatalysis in enhancing our understanding of tryptamine biosynthesis and facilitating the production of high-purity psilocybin and other tryptamines for therapeutic and research use.
{"title":"Exploring the biocatalysis of psilocybin and other tryptamines: Enzymatic pathways, synthetic strategies, and industrial implications.","authors":"Lucas Henrique Junges, Marcelo Müller-Santos","doi":"10.1002/btpr.3513","DOIUrl":"10.1002/btpr.3513","url":null,"abstract":"<p><p>Tryptamines play diverse roles as neurotransmitters and psychoactive compounds found in various organisms. Psilocybin, a notable tryptamine, has garnered attention for its therapeutic potential in treating mental health disorders like depression and anxiety. Despite its promising applications, current extraction methods for psilocybin are labor-intensive and economically limiting. We suggest biocatalysis as a sustainable alternative, leveraging enzymes to synthesize psilocybin and other tryptamines efficiently. By elucidating psilocybin biosynthesis pathways, researchers aim to advance synthetic methodologies and industrial applications. This review underscores the transformative potential of biocatalysis in enhancing our understanding of tryptamine biosynthesis and facilitating the production of high-purity psilocybin and other tryptamines for therapeutic and research use.</p>","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":" ","pages":"e3513"},"PeriodicalIF":2.5,"publicationDate":"2024-10-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142375026","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Daphne Keulen, Tim Neijenhuis, Adamantia Lazopoulou, Roxana Disela, Geoffroy Geldhof, Olivier Le Bussy, Marieke E Klijn, Marcel Ottens
Optimizing a biopharmaceutical chromatographic purification process is currently the greatest challenge during process development. A lack of process understanding calls for extensive experimental efforts in pursuit of an optimal process. In silico techniques, such as mechanistic or data driven modeling, enhance the understanding, allowing more cost-effective and time efficient process optimization. This work presents a modeling strategy integrating quantitative structure property relationship (QSPR) models and chromatographic mechanistic models (MM) to optimize a cation exchange (CEX) capture step, limiting experiments. In QSPR, structural characteristics obtained from the protein structure are used to describe physicochemical behavior. This QSPR information can be applied in MM to predict the chromatogram and optimize the entire process. To validate this approach, retention profiles of six proteins were determined experimentally from mixtures, at different pH (3.5, 4.3, 5.0, and 7.0). Four proteins at different pH's were used to train QSPR models predicting the retention volumes and characteristic charge, subsequently the equilibrium constant was determined. For an unseen protein knowing only the protein structure, the retention peak difference between the modeled and experimental peaks was 0.2% relative to the gradient length (60 column volume). Next, the CEX capture step was optimized, demonstrating a consistent result in both the experimental and QSPR-based methods. The impact of model parameter confidence on the final optimization revealed two viable process conditions, one of which is similar to the optimization achieved using experimentally obtained parameters. The multiscale modeling approach reduces the required experimental effort by identification of initial process conditions, which can be optimized.
{"title":"From protein structure to an optimized chromatographic capture step using multiscale modeling.","authors":"Daphne Keulen, Tim Neijenhuis, Adamantia Lazopoulou, Roxana Disela, Geoffroy Geldhof, Olivier Le Bussy, Marieke E Klijn, Marcel Ottens","doi":"10.1002/btpr.3505","DOIUrl":"https://doi.org/10.1002/btpr.3505","url":null,"abstract":"<p><p>Optimizing a biopharmaceutical chromatographic purification process is currently the greatest challenge during process development. A lack of process understanding calls for extensive experimental efforts in pursuit of an optimal process. In silico techniques, such as mechanistic or data driven modeling, enhance the understanding, allowing more cost-effective and time efficient process optimization. This work presents a modeling strategy integrating quantitative structure property relationship (QSPR) models and chromatographic mechanistic models (MM) to optimize a cation exchange (CEX) capture step, limiting experiments. In QSPR, structural characteristics obtained from the protein structure are used to describe physicochemical behavior. This QSPR information can be applied in MM to predict the chromatogram and optimize the entire process. To validate this approach, retention profiles of six proteins were determined experimentally from mixtures, at different pH (3.5, 4.3, 5.0, and 7.0). Four proteins at different pH's were used to train QSPR models predicting the retention volumes and characteristic charge, subsequently the equilibrium constant was determined. For an unseen protein knowing only the protein structure, the retention peak difference between the modeled and experimental peaks was 0.2% relative to the gradient length (60 column volume). Next, the CEX capture step was optimized, demonstrating a consistent result in both the experimental and QSPR-based methods. The impact of model parameter confidence on the final optimization revealed two viable process conditions, one of which is similar to the optimization achieved using experimentally obtained parameters. The multiscale modeling approach reduces the required experimental effort by identification of initial process conditions, which can be optimized.</p>","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":" ","pages":"e3505"},"PeriodicalIF":2.5,"publicationDate":"2024-09-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142340452","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Sebastian-Juan Reyes, Phuong Lan Pham, Yves Durocher, Olivier Henry
Technology scale-up and transfer are a fundamental and critical part of process development in biomanufacturing. Important bioreactor hydrodynamic characteristics such as working volume, overhead gas flow rate, volumetric power input (P/V), impeller type, agitation regimen, sparging aeration strategy, sparger type, and kLa must be selected based on key performance indicators (KPI) to ensure a smooth and seamless process scale-up and transfer. Finding suitable operational setpoints and developing an efficient feeding regimen to ensure process efficacy and consistency are instrumental. In this investigation, process development of a cumate inducible Chinese hamster ovary (CHO) stable pool expressing trimeric SARS-CoV-2 spike protein in 1.8 L benchtop stirred-tank bioreactors is detailed. Various dissolved oxygen levels and aeration air caps were studied to determine their impact on cell growth and metabolism, culture longevity, and endpoint product titers. Once hydrodynamic conditions were tuned to an optimal zone, various feeding strategies were explored to increase culture performance. Dynamic feedings such as feeding based on current culture volume, viable cell density (VCD), oxygen uptake rate (OUR), and bio-capacitance signals were tested and compared to standard bolus addition. Increases in integral of viable cell concentration (IVCC) (1.25-fold) and protein yield (2.52-fold), as well as greater culture longevity (extension of 5 days) were observed in dynamic feeding strategies when compared to periodic bolus feeding. Our study emphasizes the benefits of designing feeding strategies around metabolically relevant signals such as OUR and bio-capacitance signals.
{"title":"CHO stable pool fed-batch process development of SARS-CoV-2 spike protein production: Impact of aeration conditions and feeding strategies.","authors":"Sebastian-Juan Reyes, Phuong Lan Pham, Yves Durocher, Olivier Henry","doi":"10.1002/btpr.3507","DOIUrl":"https://doi.org/10.1002/btpr.3507","url":null,"abstract":"<p><p>Technology scale-up and transfer are a fundamental and critical part of process development in biomanufacturing. Important bioreactor hydrodynamic characteristics such as working volume, overhead gas flow rate, volumetric power input (P/V), impeller type, agitation regimen, sparging aeration strategy, sparger type, and k<sub>L</sub>a must be selected based on key performance indicators (KPI) to ensure a smooth and seamless process scale-up and transfer. Finding suitable operational setpoints and developing an efficient feeding regimen to ensure process efficacy and consistency are instrumental. In this investigation, process development of a cumate inducible Chinese hamster ovary (CHO) stable pool expressing trimeric SARS-CoV-2 spike protein in 1.8 L benchtop stirred-tank bioreactors is detailed. Various dissolved oxygen levels and aeration air caps were studied to determine their impact on cell growth and metabolism, culture longevity, and endpoint product titers. Once hydrodynamic conditions were tuned to an optimal zone, various feeding strategies were explored to increase culture performance. Dynamic feedings such as feeding based on current culture volume, viable cell density (VCD), oxygen uptake rate (OUR), and bio-capacitance signals were tested and compared to standard bolus addition. Increases in integral of viable cell concentration (IVCC) (1.25-fold) and protein yield (2.52-fold), as well as greater culture longevity (extension of 5 days) were observed in dynamic feeding strategies when compared to periodic bolus feeding. Our study emphasizes the benefits of designing feeding strategies around metabolically relevant signals such as OUR and bio-capacitance signals.</p>","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":" ","pages":"e3507"},"PeriodicalIF":2.5,"publicationDate":"2024-09-27","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142340451","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Winne F S M Silva, Ludovico Migliolo, Patrícia S Silva, Glaucia M S Lima, Maria D L Oliveira, Cesar A S Andrade
Healthcare-associated infections (HAIs) pose significant challenges to global health due to pathogen complexity and antimicrobial resistance. Biosensors utilizing antimicrobial peptides offer innovative solutions. Hylarana picturata Multiple Active Peptide 1 (Hp-MAP1), derived from Temporin-PTA, exhibits antibacterial properties sourced from the skin secretions of the Malaysian fire-bellied frog. An innovative sensing layer was developed for the electrochemical biorecognition of diverse pathogens: Pseudomonas aeruginosa, Klebsiella pneumoniae, Escherichia coli, and Staphylococcus aureus. Electrochemical impedance spectroscopy differentiated microorganisms based on distinct electrochemical responses. The sensor layer, composed of functionalized multi-walled carbon nanotubes (MWCNTs) associated with Hp-MAP1, exhibited varying levels of charge transfer resistance (RCT) for different microorganisms. Gram-negative species, especially P. aeruginosa, displayed higher RCT values, indicating better impedimetric responses. Excellent LODs were observed for P. aeruginosa (0.60), K. pneumoniae (0.42), E. coli (0.67), and S. aureus (0.59), highlighting the efficacy of the MWCNTs/Hp-MAP1 biosensor in microbial identification. The MWCNTs/Hp-MAP1 biosensor platform presents a promising and effective microbial identification strategy with potential healthcare applications to mitigate HAIs and enhance patient care.
{"title":"Nanosensor based on HP-MAP1 and carbon nanotubes for bacteria detection.","authors":"Winne F S M Silva, Ludovico Migliolo, Patrícia S Silva, Glaucia M S Lima, Maria D L Oliveira, Cesar A S Andrade","doi":"10.1002/btpr.3510","DOIUrl":"https://doi.org/10.1002/btpr.3510","url":null,"abstract":"<p><p>Healthcare-associated infections (HAIs) pose significant challenges to global health due to pathogen complexity and antimicrobial resistance. Biosensors utilizing antimicrobial peptides offer innovative solutions. Hylarana picturata Multiple Active Peptide 1 (Hp-MAP1), derived from Temporin-PTA, exhibits antibacterial properties sourced from the skin secretions of the Malaysian fire-bellied frog. An innovative sensing layer was developed for the electrochemical biorecognition of diverse pathogens: Pseudomonas aeruginosa, Klebsiella pneumoniae, Escherichia coli, and Staphylococcus aureus. Electrochemical impedance spectroscopy differentiated microorganisms based on distinct electrochemical responses. The sensor layer, composed of functionalized multi-walled carbon nanotubes (MWCNTs) associated with Hp-MAP1, exhibited varying levels of charge transfer resistance (R<sub>CT</sub>) for different microorganisms. Gram-negative species, especially P. aeruginosa, displayed higher R<sub>CT</sub> values, indicating better impedimetric responses. Excellent LODs were observed for P. aeruginosa (0.60), K. pneumoniae (0.42), E. coli (0.67), and S. aureus (0.59), highlighting the efficacy of the MWCNTs/Hp-MAP1 biosensor in microbial identification. The MWCNTs/Hp-MAP1 biosensor platform presents a promising and effective microbial identification strategy with potential healthcare applications to mitigate HAIs and enhance patient care.</p>","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":" ","pages":"e3510"},"PeriodicalIF":2.5,"publicationDate":"2024-09-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142340453","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Piyush Agarwal, Chris McCready, Say Kong Ng, Jake Chng Ng, Jeroen van de Laar, Maarten Pennings, Gerben Zijlstra
The bio‐pharmaceutical industry heavily relies on mammalian cells for the production of bio‐therapeutic proteins. The complexity of implementing and high cost‐of‐goods of these processes are currently limiting more widespread patient access. This is driving efforts to enhance cell culture productivity and cost reduction. Upstream process intensification (PI), using perfusion approaches in the seed train and/or the main bioreactor, has shown substantial promise to enhance productivity. However, developing optimal process conditions for perfusion‐based processes remain challenging due to resource and time constraints. Model‐based optimization offers a solution by systematically screening process parameters like temperature, pH, and culture media to find the optimum conditions in silico. To our knowledge, this is the first experimentally validated model to explain the perfusion dynamics under different operating conditions and scales for process optimization. The hybrid model accurately describes Chinese hamster ovary (CHO) cell culture growth dynamics and a neural network model explains the production of mAb, allowing for optimization of media exchange rates. Results from six perfusion runs in Ambr® 250 demonstrated high accuracy, confirming the model's utility. Further, the implementation of dynamic media exchange rate schedule determined through model‐based optimization resulted in 50% increase in volumetric productivity. Additionally, two 5 L‐scale experiments validated the model's reliable extrapolation capabilities to large bioreactors. This approach could reduce the number of wet lab experiments needed for culture process optimization, offering a promising avenue for improving productivity, cost‐of‐goods in bio‐pharmaceutical manufacturing, in turn improving patient access to pivotal medicine.
生物制药行业严重依赖哺乳动物细胞来生产生物治疗蛋白。目前,实施这些工艺的复杂性和高昂的商品成本限制了患者更广泛地使用这些工艺。这推动了提高细胞培养生产率和降低成本的努力。在种子系和/或主生物反应器中使用灌流方法进行上游工艺强化(PI),已显示出提高生产率的巨大前景。然而,由于资源和时间的限制,为基于灌流的工艺开发最佳工艺条件仍具有挑战性。基于模型的优化提供了一种解决方案,即通过系统筛选温度、pH 值和培养基等工艺参数,找到最佳的硅学条件。据我们所知,这是首个经过实验验证的模型,用于解释不同操作条件和规模下的灌流动态,以实现工艺优化。该混合模型准确地描述了中国仓鼠卵巢(CHO)细胞培养的生长动态,神经网络模型则解释了 mAb 的生产,从而实现了培养基交换率的优化。在 Ambr® 250 中进行的六次灌流运行结果表明,该模型具有很高的准确性,证实了其实用性。此外,通过基于模型的优化确定的动态培养基交换率计划的实施使体积生产率提高了 50%。此外,两个 5 升规模的实验验证了该模型对大型生物反应器的可靠外推能力。这种方法可以减少培养过程优化所需的湿实验室实验数量,为提高生物制药生产的生产率和产品成本提供了一条很有前景的途径,进而改善了患者获得关键药物的机会。
{"title":"Hybrid modeling for in silico optimization of a dynamic perfusion cell culture process","authors":"Piyush Agarwal, Chris McCready, Say Kong Ng, Jake Chng Ng, Jeroen van de Laar, Maarten Pennings, Gerben Zijlstra","doi":"10.1002/btpr.3503","DOIUrl":"https://doi.org/10.1002/btpr.3503","url":null,"abstract":"The bio‐pharmaceutical industry heavily relies on mammalian cells for the production of bio‐therapeutic proteins. The complexity of implementing and high cost‐of‐goods of these processes are currently limiting more widespread patient access. This is driving efforts to enhance cell culture productivity and cost reduction. Upstream process intensification (PI), using perfusion approaches in the seed train and/or the main bioreactor, has shown substantial promise to enhance productivity. However, developing optimal process conditions for perfusion‐based processes remain challenging due to resource and time constraints. Model‐based optimization offers a solution by systematically screening process parameters like temperature, pH, and culture media to find the optimum conditions in silico. To our knowledge, this is the first experimentally validated model to explain the perfusion dynamics under different operating conditions and scales for process optimization. The hybrid model accurately describes Chinese hamster ovary (CHO) cell culture growth dynamics and a neural network model explains the production of mAb, allowing for optimization of media exchange rates. Results from six perfusion runs in Ambr® 250 demonstrated high accuracy, confirming the model's utility. Further, the implementation of dynamic media exchange rate schedule determined through model‐based optimization resulted in 50% increase in volumetric productivity. Additionally, two 5 L‐scale experiments validated the model's reliable extrapolation capabilities to large bioreactors. This approach could reduce the number of wet lab experiments needed for culture process optimization, offering a promising avenue for improving productivity, cost‐of‐goods in bio‐pharmaceutical manufacturing, in turn improving patient access to pivotal medicine.","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":"54 1","pages":"e3503"},"PeriodicalIF":2.9,"publicationDate":"2024-09-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142266024","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Cristina A. T. Silva, Amine A. Kamen, Olivier Henry
Vesicular stomatitis virus (VSV) has been increasingly demonstrated as a promising viral vector platform. As the interest over this modality for vaccine and gene therapy applications increases, the need for intensified processes to produce these vectors emerge. In this study, we develop fed‐batch‐based operations to intensify the production of a recombinant VSV‐based vaccine candidate (rVSV‐SARS‐CoV‐2) in suspension cultures of HEK293 cells. A feeding strategy, in which a commercial concentrated medium was added to cultures based on cell growth through a fixed cell specific feeding rate (CSFR), was applied for the development of two different processes using Ambr250 modular bioreactors. Cultures operated in hybrid fed‐batch/perfusion (FB/P) or fed‐batch (FB) were able to sustain infections performed at 8.0 × 106 cells/mL, respectively resulting in 3.9 and 5.0‐fold increase in total yield (YT) and 1.7 and 5.6‐fold increase in volumetric productivity (VP) when compared with a batch reference. A maximum viral titer of 4.5 × 1010 TCID50/mL was reached, which is comparable or higher than other processes for VSV production in different cell lines. Overall, our study reports efficient fed‐batch options to intensify the production of a rVSV‐based vaccine candidate in suspension HEK293 cells.
{"title":"Fed‐batch strategies for intensified rVSV vector production in high cell density cultures of suspension HEK293 cells","authors":"Cristina A. T. Silva, Amine A. Kamen, Olivier Henry","doi":"10.1002/btpr.3506","DOIUrl":"https://doi.org/10.1002/btpr.3506","url":null,"abstract":"Vesicular stomatitis virus (VSV) has been increasingly demonstrated as a promising viral vector platform. As the interest over this modality for vaccine and gene therapy applications increases, the need for intensified processes to produce these vectors emerge. In this study, we develop fed‐batch‐based operations to intensify the production of a recombinant VSV‐based vaccine candidate (rVSV‐SARS‐CoV‐2) in suspension cultures of HEK293 cells. A feeding strategy, in which a commercial concentrated medium was added to cultures based on cell growth through a fixed cell specific feeding rate (CSFR), was applied for the development of two different processes using Ambr250 modular bioreactors. Cultures operated in hybrid fed‐batch/perfusion (FB/P) or fed‐batch (FB) were able to sustain infections performed at 8.0 × 10<jats:sup>6</jats:sup> cells/mL, respectively resulting in 3.9 and 5.0‐fold increase in total yield (<jats:italic>Y</jats:italic><jats:sub>T</jats:sub>) and 1.7 and 5.6‐fold increase in volumetric productivity (VP) when compared with a batch reference. A maximum viral titer of 4.5 × 10<jats:sup>10</jats:sup> TCID<jats:sub>50</jats:sub>/mL was reached, which is comparable or higher than other processes for VSV production in different cell lines. Overall, our study reports efficient fed‐batch options to intensify the production of a rVSV‐based vaccine candidate in suspension HEK293 cells.","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":"4 1","pages":""},"PeriodicalIF":2.9,"publicationDate":"2024-09-17","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142266025","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Victor Pasquier, Kevin Botelho Ferreira, Morgane Lergenmuller, Alexis Tottoli, Arnaud Perilleux, Jonathan Souquet, Jean-Marc Bielser
Membrane chromatography devices are a viable alternative to packed-bed resins and enable highly productive purification cascades for monoclonal antibodies and Fc-fusion proteins. In this study, ion exchange and protein A membrane chromatography performances were assessed and compared with their resin counterparts. Protein A dynamic binding capacities were higher than 50 g/L for two of the tested membranes and with a residence time of 0.2 min. For polishing, it was observed that aggregate clearance was generally less performant with membrane separation when compared to resins with similar ligands. However, the comparable yield and increased productivity of membranes could be enough to consider their implementation. In addition, lifetime studies demonstrated that the performance of membranes remained robust over cycles. One hundred cycles were reached for most of the tested membranes with no impact on the process performance nor product quality. Finally, purification cascades were fully operated with membranes, from capture to polishing, reaching good levels of host cells proteins (less than 50 ppm) and aggregates (equal to or less than 1%). The outcome of this study demonstrated that resin chromatography could be fully replaced by membranes for monoclonal antibody and Fc-fusion protein purification processes.
膜层析装置是填料床树脂的可行替代品,可实现单克隆抗体和 Fc 融合蛋白的高产纯化级联。本研究评估了离子交换和蛋白 A 膜层析的性能,并将其与同类树脂进行了比较。其中两种测试膜的蛋白 A 动态结合能力高于 50 克/升,停留时间为 0.2 分钟。在抛光方面,与具有类似配体的树脂相比,聚合体清除率通常低于膜分离性能。然而,膜的产量和生产率的提高足以让我们考虑使用膜。此外,寿命研究表明,膜的性能在循环过程中保持稳定。大多数测试膜都达到了一百次循环,对工艺性能和产品质量没有影响。最后,从捕获到抛光,纯化级联完全用膜操作,宿主细胞蛋白质(小于 50 ppm)和聚集物(等于或小于 1%)达到良好水平。这项研究结果表明,在单克隆抗体和 Fc 融合蛋白纯化过程中,膜完全可以取代树脂色谱法。
{"title":"Assessment of membrane-based downstream purification processes as a replacement to traditional resin bead for monoclonal antibody purification.","authors":"Victor Pasquier, Kevin Botelho Ferreira, Morgane Lergenmuller, Alexis Tottoli, Arnaud Perilleux, Jonathan Souquet, Jean-Marc Bielser","doi":"10.1002/btpr.3508","DOIUrl":"https://doi.org/10.1002/btpr.3508","url":null,"abstract":"<p><p>Membrane chromatography devices are a viable alternative to packed-bed resins and enable highly productive purification cascades for monoclonal antibodies and Fc-fusion proteins. In this study, ion exchange and protein A membrane chromatography performances were assessed and compared with their resin counterparts. Protein A dynamic binding capacities were higher than 50 g/L for two of the tested membranes and with a residence time of 0.2 min. For polishing, it was observed that aggregate clearance was generally less performant with membrane separation when compared to resins with similar ligands. However, the comparable yield and increased productivity of membranes could be enough to consider their implementation. In addition, lifetime studies demonstrated that the performance of membranes remained robust over cycles. One hundred cycles were reached for most of the tested membranes with no impact on the process performance nor product quality. Finally, purification cascades were fully operated with membranes, from capture to polishing, reaching good levels of host cells proteins (less than 50 ppm) and aggregates (equal to or less than 1%). The outcome of this study demonstrated that resin chromatography could be fully replaced by membranes for monoclonal antibody and Fc-fusion protein purification processes.</p>","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":" ","pages":"e3508"},"PeriodicalIF":2.5,"publicationDate":"2024-09-16","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142280026","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Vaibhav Srivastava, Aditya P Sarnaik, Pramod P Wangikar
Alkanes are high-energy hydrocarbons that are foreseen as next generation biofuels. Cyanobacteria are known to naturally synthesize C15-C19 alkanes; however, the titers are too low to make this a commercially viable process. Therefore, to leverage these photosynthetic platforms for improved alkane production, here we engineered three novel isolates of Synechococcus elongatus PCC 11801, PCC 11802, and IITB6. The two gene AAR-ADO alkane biosynthesis pathway was constructed by cloning the genes for acyl-ACP reductase (aar) and aldehyde deformylating oxygenase (ado) from S. elongatus PCC 7942 under the regulation of PrbcL promoter from PCC 7942 and native promoters from PCC 11801 such as PcpcB300, PpsbAI, and PpsbAIII. The genes were separately cloned under two different promoters, creating a library of the engineered strains. The results indicated that the engineered strains of novel S. elongatus isolates produced significantly higher amounts of alkanes than the model strain PCC 7942. The highest alkane yield achieved was 4.1 mg/gDCW in BG-11, while the highest titer was 31.5 mg/L in 5X BG-11, with an engineered IITB6 strain (PcpcB300:aar:TrrnB::PrbcL:ado:TLac). Overall, the study highlights the potential of newly isolated S. elongatus strains as efficient alkane production platforms.
{"title":"Metabolic engineering of rapidly growing Synechococcus elongatus strains for phototrophic production of alkanes.","authors":"Vaibhav Srivastava, Aditya P Sarnaik, Pramod P Wangikar","doi":"10.1002/btpr.3509","DOIUrl":"https://doi.org/10.1002/btpr.3509","url":null,"abstract":"<p><p>Alkanes are high-energy hydrocarbons that are foreseen as next generation biofuels. Cyanobacteria are known to naturally synthesize C15-C19 alkanes; however, the titers are too low to make this a commercially viable process. Therefore, to leverage these photosynthetic platforms for improved alkane production, here we engineered three novel isolates of Synechococcus elongatus PCC 11801, PCC 11802, and IITB6. The two gene AAR-ADO alkane biosynthesis pathway was constructed by cloning the genes for acyl-ACP reductase (aar) and aldehyde deformylating oxygenase (ado) from S. elongatus PCC 7942 under the regulation of P<sub>rbcL</sub> promoter from PCC 7942 and native promoters from PCC 11801 such as P<sub>cpcB300</sub>, P<sub>psbAI</sub>, and P<sub>psbAIII</sub>. The genes were separately cloned under two different promoters, creating a library of the engineered strains. The results indicated that the engineered strains of novel S. elongatus isolates produced significantly higher amounts of alkanes than the model strain PCC 7942. The highest alkane yield achieved was 4.1 mg/gDCW in BG-11, while the highest titer was 31.5 mg/L in 5X BG-11, with an engineered IITB6 strain (P<sub>cpcB300</sub>:aar:T<sub>rrnB</sub>::P<sub>rbcL</sub>:ado:T<sub>Lac</sub>). Overall, the study highlights the potential of newly isolated S. elongatus strains as efficient alkane production platforms.</p>","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":" ","pages":"e3509"},"PeriodicalIF":2.5,"publicationDate":"2024-09-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142280027","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Off-the-shelf cell therapies hold significant curative potential for conditions, such as Parkinson's disease and heart failure. However, these therapies face unique cryopreservation challenges, especially when novel routes of administration, such as intracerebral or epicardial injection, require cryopreservation media that are safe for direct post-thaw administration. Current practices often involve post-thaw washing to remove dimethyl sulfoxide (Me2SO), a cytotoxic cryoprotective agent, which complicates the development and clinical translation of off-the-shelf therapies. To overcome these obstacles, there is a critical need to explore Me2SO-free cryopreservation methods. While such methods typically yield suboptimal post-thaw viability with conventional slow-freeze protocols, optimizing freezing profiles offers a promising strategy to enhance their performance. This comprehensive review examines the latest advancements in cryopreservation techniques across various cell therapy platforms, with a specific case study of iPSC-derived therapies used to illustrate the scalability challenges. By identifying key thermodynamic and biochemical phenomena that occur during freezing, this review aims to identify cell-type independent approaches to improve the efficiency and efficacy of cryopreservation strategies, thereby supporting the widespread adoption and clinical success of off-the-shelf cell therapies.
{"title":"Optimizing cryopreservation strategies for scalable cell therapies: A comprehensive review with insights from iPSC-derived therapies","authors":"Michael Dobruskin, Geoffrey Toner, Ronald Kander","doi":"10.1002/btpr.3504","DOIUrl":"10.1002/btpr.3504","url":null,"abstract":"<p>Off-the-shelf cell therapies hold significant curative potential for conditions, such as Parkinson's disease and heart failure. However, these therapies face unique cryopreservation challenges, especially when novel routes of administration, such as intracerebral or epicardial injection, require cryopreservation media that are safe for direct post-thaw administration. Current practices often involve post-thaw washing to remove dimethyl sulfoxide (Me<sub>2</sub>SO), a cytotoxic cryoprotective agent, which complicates the development and clinical translation of off-the-shelf therapies. To overcome these obstacles, there is a critical need to explore Me<sub>2</sub>SO-free cryopreservation methods. While such methods typically yield suboptimal post-thaw viability with conventional slow-freeze protocols, optimizing freezing profiles offers a promising strategy to enhance their performance. This comprehensive review examines the latest advancements in cryopreservation techniques across various cell therapy platforms, with a specific case study of iPSC-derived therapies used to illustrate the scalability challenges. By identifying key thermodynamic and biochemical phenomena that occur during freezing, this review aims to identify cell-type independent approaches to improve the efficiency and efficacy of cryopreservation strategies, thereby supporting the widespread adoption and clinical success of off-the-shelf cell therapies.</p>","PeriodicalId":8856,"journal":{"name":"Biotechnology Progress","volume":"40 6","pages":""},"PeriodicalIF":2.5,"publicationDate":"2024-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://onlinelibrary.wiley.com/doi/epdf/10.1002/btpr.3504","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142266026","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":3,"RegionCategory":"生物学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}